JPH07159079A - Heat exchanging device - Google Patents

Heat exchanging device

Info

Publication number
JPH07159079A
JPH07159079A JP5305093A JP30509393A JPH07159079A JP H07159079 A JPH07159079 A JP H07159079A JP 5305093 A JP5305093 A JP 5305093A JP 30509393 A JP30509393 A JP 30509393A JP H07159079 A JPH07159079 A JP H07159079A
Authority
JP
Japan
Prior art keywords
exhaust gas
combustion exhaust
water pipe
heat exchange
combustion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP5305093A
Other languages
Japanese (ja)
Other versions
JP2729461B2 (en
Inventor
Masaaki Nakaura
雅昭 中浦
Kazuo Yagi
和男 八木
Koji Yano
宏治 矢野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Rinnai Corp
Original Assignee
Rinnai Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rinnai Corp filed Critical Rinnai Corp
Priority to JP5305093A priority Critical patent/JP2729461B2/en
Publication of JPH07159079A publication Critical patent/JPH07159079A/en
Application granted granted Critical
Publication of JP2729461B2 publication Critical patent/JP2729461B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To raise a heat efficiency by providing a first exhaust gas convergence means for collecting a combustion exhaust gas on a surface of the upstream side of a flow of the exhaust gas with respect to a water passing tube, and a second exhaust gas convergence means for exhausting the combustion exhaust gas from the first exhaust gas convergence means after collecting it at the downstream side surface of the exhaust gas flow with respect to the water passing tube. CONSTITUTION:As guide plates 5, 5 are each other made to be in a closely contact state, a combustion exhaust gas sent into a heat exchanging section 1b executes an inflow from an open section 51, contacts the upper face of a water passing tube 11 and executes an inflow among a guide plate 5, a water passing tube 11 and a fin 12. This combustion exhaust gas is exhausted from an open section 52 at the underside direction of the water passing tube 11, and contacts the underface of the water passing tube 11 at this time. Accordingly, a combustion gas is condensed, in a heat exchanging section 1b, by a contact action of the combustion exhaust gas over all circumferential periphery of the water passing tube 11 and the fin 12 and a heat efficiency is raised. A drain adhering to the upper section of an outside wall of the guide plate 5 enters the inside through a pierced hole 55 and flows downwards from the open section 52.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、燃焼装置からの排気通
路に吸熱用の通水管を配置した熱交換装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchange device having a heat absorbing water pipe arranged in an exhaust passage from a combustion device.

【0002】[0002]

【従来技術及びその課題】燃焼排気からの熱交換効率の
向上を図った熱交換装置として、図7に示すように、ガ
スバーナ(3) と二段式の熱交換器(1) とが組み合わされ
たものがある。前記熱交換器(1) は、通水管(11)とその
外周に設けられた多数のフィン(12)(12)とこれらを収容
する缶体(6) とから構成されており、該熱交換器(1) は
通水管(11)の下流側の主としてガスバーナ(3) の燃焼排
気の顕熱を吸熱する主熱交換部(1a)と、その下方に配設
された通水管(11)の上流側の主としてガスバーナ(3) の
燃焼排気の潜熱を吸熱する副熱交換部(1b)とから構成さ
れる。そして、熱交換器(1) の下方には、該熱交換器
(1) に付着するドレンを外部に排出するためのドレン排
出口(8) が設けられている。
2. Description of the Related Art As shown in FIG. 7, a gas burner (3) and a two-stage heat exchanger (1) are combined as a heat exchange device for improving the efficiency of heat exchange from combustion exhaust gas. There is something. The heat exchanger (1) is composed of a water pipe (11), a large number of fins (12) (12) provided on the outer periphery of the water pipe (11), and a can body (6) accommodating them. The device (1) consists of a main heat exchange part (1a) that absorbs the sensible heat of the combustion exhaust of the gas burner (3) on the downstream side of the water pipe (11) and a water pipe (11) arranged below it. It is mainly composed of an auxiliary heat exchange part (1b) which absorbs latent heat of combustion exhaust gas of the gas burner (3) on the upstream side. And below the heat exchanger (1), the heat exchanger
A drain discharge port (8) is provided for discharging the drain attached to (1) to the outside.

【0003】前記ガスバーナ(3) の炎孔部は下向きに設
定され、その炎形成域近傍に前記主熱交換部(1a)が位置
するように配設されている。そして、前記ガスバーナ
(3) にはファン(4) によって強制的に燃焼用空気が押し
込み供給されるようになっており、これにより、ガスバ
ーナの燃焼排気は主・副熱交換部(1a)(1b)を通過した
後、これの下方の排気筒(21)を介して外部に排出される
ようになっている。
The flame hole portion of the gas burner (3) is set downward, and the main heat exchange portion (1a) is arranged near the flame forming region. And the gas burner
Combustion air is forced to be supplied to (3) by a fan (4), which allows the combustion exhaust of the gas burner to pass through the main and auxiliary heat exchange sections (1a) and (1b). After that, the gas is discharged to the outside through the exhaust pipe (21) below this.

【0004】このものでは、ガスバーナ(3) を燃焼させ
て副熱交換部(1b)側に位置する通水管(11)から水道水を
供給すると、該通水管(11)内の通水は、ガスバーナ(3)
の発生熱量を通水管(11)やフィン(12)(12)から吸熱し
て、湯となって主熱交換部(1a)から外部に取り出される
が、そのための吸熱作用の中で、主熱交換部(1a)では主
として、ガスバーナ(3) の燃焼排気の顕熱を吸熱する作
用が行われ、副熱交換部(1b)では、主として、ガスバー
ナ(3) の燃焼排気中の水蒸気を凝縮させてその潜熱を吸
熱する作用が行われる。即ち、副熱交換部(1b)では、顕
熱が奪われて冷却された燃焼排気をその露点温度以下に
冷却させることによってドレンを発生させ、そのときの
潜熱を該副熱交換部(1b)における通水管(11)内の通水に
吸熱させているのである。そして、前記副熱交換部(1b)
に付着したドレンは、その自重によって該副熱交換部(1
b)の下方に滴下し、ドレン排出口(8) から外部に排出さ
れる。このものでは、燃焼排気の顕熱だけでなく潜熱を
も積極的に熱交換部に吸収させるので、熱効率が向上す
るという利点がある。
In this case, when the gas burner (3) is burned and tap water is supplied from the water pipe (11) located on the side of the sub heat exchange portion (1b), the water in the water pipe (11) is Gas burner (3)
The amount of heat generated by the heat is absorbed from the water pipes (11) and fins (12) (12), and becomes hot water that is taken out from the main heat exchange section (1a) to the outside. The exchange section (1a) mainly acts to absorb the sensible heat of the combustion exhaust gas of the gas burner (3), and the auxiliary heat exchange section (1b) mainly condenses water vapor in the combustion exhaust gas of the gas burner (3). The latent heat is absorbed. That is, in the sub heat exchange section (1b), drainage is generated by cooling the sensible heat depleted and cooled combustion exhaust gas to a temperature below its dew point temperature, and latent heat at that time is generated to the sub heat exchange section (1b). The water in the water pipe (11) in the is absorbing heat. And the sub heat exchange section (1b)
The drain attached to the sub-heat exchange section (1
It drips below b) and is discharged to the outside from the drain discharge port (8). In this case, not only the sensible heat of the combustion exhaust gas but also the latent heat is positively absorbed in the heat exchange section, so that there is an advantage that the thermal efficiency is improved.

【0005】しかしながら、このものでは、熱効率を未
だ十分に向上させることができない。熱交換器(1) に送
り込まれる燃焼排気は、該熱交換器(1) における通水管
(11)の部分及びこれら通水管の相互間の間隔に対して均
等に流入するために、ガスバーナ(3) からの燃焼排気の
全てが通水管(11)の上面に接触しない。又、通水管(11)
の下面側は排気流の流れにおいて背後にあたるために、
該下面側では燃焼排気が淀んだ状態になり、当該部分に
新鮮な燃焼排気が流れ込まない。これらのことから、燃
焼排気の全てが通水管(11)に有効に接触して熱交換する
こととはならず、この点で熱効率を十分には向上させる
ことができない。
However, this one cannot sufficiently improve the thermal efficiency. Combustion exhaust gas sent to the heat exchanger (1) is a water pipe in the heat exchanger (1).
All of the combustion exhaust gas from the gas burner (3) does not come into contact with the upper surface of the water pipe (11) because it flows evenly into the portion (11) and the space between these water pipes. Also, water pipe (11)
Because the lower surface side of is behind in the flow of the exhaust flow,
The combustion exhaust gas stagnates on the lower surface side, and fresh combustion exhaust gas does not flow into the relevant portion. For these reasons, not all of the combustion exhaust gas comes into effective contact with the water pipe (11) for heat exchange, and in this respect, the thermal efficiency cannot be sufficiently improved.

【0006】尚、上記と同様の不都合は、図8に示すよ
うに、ガスバーナ(3) 上方の燃焼排気通路の下流側に熱
交換器(1) が配設される形式のものでも発生する。本発
明は、このような、『燃焼装置からの排気通路に吸熱用
の通水管(11)を設けた構成の熱交換装置』において、熱
効率を向上させることをその課題とする。 [請求項1の発明について]
The same inconvenience as described above also occurs in the type in which the heat exchanger (1) is arranged on the downstream side of the combustion exhaust passage above the gas burner (3) as shown in FIG. An object of the present invention is to improve the thermal efficiency in such a “heat exchange device having a water passage pipe (11) for absorbing heat in the exhaust passage from the combustion device”. [Invention of Claim 1]

【0007】[0007]

【技術的手段】上記課題を解決するために講じた本発明
の技術的手段は、『通水管(11)における排気流の上流側
の表面に燃焼排気を集めるための第1排気集中手段(A)
と、該第1排気集中手段(A) からの燃焼排気を通水管(1
1)における排気流の下流側表面に集めて排出するための
第2排気集中手段(B) とを具備させた』ことである。
[Technical Means] The technical means of the present invention taken to solve the above-mentioned problems are as follows: "First exhaust gas concentrating means (A) for collecting combustion exhaust gas on the surface of the water flow pipe (11) on the upstream side of the exhaust gas flow. )
And combustion exhaust gas from the first exhaust gas concentration means (A) (1
The second exhaust gas concentrating means (B) for collecting and discharging the exhaust gas flow on the downstream surface in 1) is provided ”.

【0008】[0008]

【作用】本発明の上記技術的手段は、次のように作用す
る。燃焼装置で生成された燃焼排気が通水管(11)に接触
し、燃焼排気中の熱量が前記通水管(11)内の通水に熱交
換される。このとき、図1の概念図に示すように、通水
管(11)に向けて流れる燃焼排気だけでなく、更にこれか
ら外れた部分に供給される燃焼排気が第1排気集中手段
(A) によって通水管(11)の部分に集められる。即ち、排
気流の上流側に面する通水管(11)の表面に向けて燃焼排
気が集められ、これにより前記通水管(11)の表面部分に
燃焼排気が集中的に吹き付けられる。そして、上記第1
排気集中手段(A) から通水管(11)の表面に吹き付けられ
た燃焼排気は、該通水管(11)の側方を流れた後に第2排
気集中手段(B) によって通水管(11)の裏面部分、即ち、
通水管(11)における排気流の下流側表面に集められた後
に排出される。このように、燃焼装置からの燃焼排気
は、通水管(11)における上流側表面に吹きつけられた
後、その側方表面から下流側表面に沿って流れ、その後
排気流下流側の表面から集中的に排出されることとな
る。このことから、上記技術的手段によれば、通水管(1
1)に接触する燃焼排気の量が多くなり、又、排気流と通
水管(11)との接触時間が長くなる。
The above technical means of the present invention operates as follows. The combustion exhaust gas generated by the combustion device contacts the water flow pipe (11), and the amount of heat in the combustion exhaust gas is exchanged with the water flow in the water flow pipe (11). At this time, as shown in the conceptual diagram of FIG. 1, not only the combustion exhaust flowing toward the water pipe (11) but also the combustion exhaust supplied to a portion further away from the water passage (11) is the first exhaust concentration means.
It will be collected in the water pipe (11) by (A). That is, the combustion exhaust gas is collected toward the surface of the water flow pipe (11) facing the upstream side of the exhaust flow, whereby the combustion exhaust gas is intensively blown to the surface portion of the water flow pipe (11). And the first
The combustion exhaust blown from the exhaust gas concentrator (A) to the surface of the water pipe (11) flows to the side of the water pipe (11) and then flows to the side of the water pipe (11) by the second exhaust gas concentrator (B). The back part, that is,
After being collected on the downstream surface of the exhaust flow in the water pipe (11), it is discharged. Thus, the combustion exhaust from the combustion device is blown to the upstream surface of the water pipe (11), then flows from the side surface to the downstream surface, and then is concentrated from the exhaust flow downstream surface. Will be discharged. From this, according to the above technical means, the water pipe (1
The amount of combustion exhaust that contacts 1) increases, and the contact time between the exhaust flow and the water pipe (11) increases.

【0009】[0009]

【効果】本発明は、上記構成であるから、次の特有の効
果を有する。通水管(11)に接触する燃焼排気の量が多く
なり、又、排気流と通水管(11)との接触時間が長くなる
から、当該熱交換装置の熱効率が向上する。 [請求項2の発明について]請求項2の発明の技術的手
段は、請求項1の発明において、『第1排気集中手段
(A) と第2排気集中手段(B) との間に通水管(11)の断面
側壁に沿って燃焼排気を案内する排気案内手段(C) を通
水管(11)の断面両側に対向配置した』ことである。
[Effect] The present invention having the above-mentioned structure has the following unique effects. Since the amount of combustion exhaust gas contacting the water flow pipe (11) increases and the contact time between the exhaust flow and the water flow pipe (11) increases, the heat efficiency of the heat exchange device is improved. [Regarding the invention of claim 2] The technical means of the invention of claim 2 is the "first exhaust gas concentrating means" in the invention of claim 1.
Exhaust guide means (C) for guiding combustion exhaust along the cross-section side wall of the water pipe (11) between (A) and the second exhaust gas concentrating means (B) are arranged on opposite sides of the water pipe (11) in cross section. I did that.

【0010】このものでは、上記請求項1の発明と同様
に、第1排気集中手段(A) 及び第2排気集中手段(B) に
よって、燃焼排気は通水管(11)における排気流の上流側
表面及び下流側表面に集められる。この場合請求項2の
発明では、通水管(11)の断面側壁に沿って燃焼排気を案
内する排気案内手段(C) を第1排気集中手段(A) と第2
排気集中手段(B) との間で通水管(11)の断面両側に対向
配置したことから、図2の概念図に示すように、前記第
1排気集中手段(A) からの燃焼排気は、排気案内手段
(C) の上流端部に供給され、通水管(11)の側方表面に沿
って確実に接触しながら、該排気案内手段(C) と通水管
(11)との間を下流端に向けて流れることとなる。
According to the present invention, as in the first aspect of the present invention, the combustion exhaust gas is upstream of the exhaust flow in the water pipe (11) by the first exhaust gas concentrating means (A) and the second exhaust gas concentrating means (B). Collected on the surface and the downstream surface. In this case, in the invention of claim 2, the exhaust gas guide means (C) for guiding the combustion exhaust gas along the side wall of the cross section of the water pipe (11) is provided with the first exhaust gas concentrating means (A) and the second exhaust gas concentrating means (A).
Since the water pipe (11) and the exhaust gas concentrating means (B) are arranged to face each other on both sides of the cross section, as shown in the conceptual diagram of FIG. 2, the combustion exhaust gas from the first exhaust gas concentrating means (A) is Exhaust guide means
(C) is supplied to the upstream end portion of the water guide pipe (11) while reliably contacting the exhaust pipe (11) and the water pipe.
It will flow toward the downstream end between (11).

【0011】したがって、このものでは、燃焼装置から
の燃焼排気が通水管(11)を通過するに際して、上記請求
項1の発明の作用に加えて、通水管(11)の側方表面には
該燃焼排気が確実に接触せしめられることから、通水管
(11)に接触する燃焼排気の量が一層多くなると共に、排
気流と通水管(11)との接触時間がより長くなるので、熱
効率が一層向上する。
Therefore, in this structure, when the combustion exhaust gas from the combustion device passes through the water pipe (11), in addition to the action of the invention of claim 1, the side surface of the water pipe (11) has Since the combustion exhaust gas is surely brought into contact with each other, the water pipe
Since the amount of combustion exhaust gas contacting (11) is further increased and the contact time between the exhaust flow and the water pipe (11) is longer, the thermal efficiency is further improved.

【0012】[0012]

【実施例】以下本発明の実施例を図面に従って説明す
る。図3に示す実施例は、燃焼排気を凝縮させてその潜
熱を吸熱する機能を備えた熱交換器(1) を具備する給湯
器に本発明を実施したものである。このものは、給湯器
本体の下部に熱交換器(1) を構成する缶体(6) を設け、
該缶体(6) の上部に多孔プレート式のガスバーナ(3) を
具備し且つ上部に給気室(42)を備える給気箱(7) を配設
したものである。そして、前記給気室(42)にはガスノズ
ル(31)を臨ませており、該給気室(42)の上部にはファン
(4) が設けられている。又、前記熱交換器(1) の下端開
口部には排気筒(21)を接続させている。
Embodiments of the present invention will be described below with reference to the drawings. In the embodiment shown in FIG. 3, the present invention is applied to a water heater having a heat exchanger (1) having a function of condensing combustion exhaust gas and absorbing its latent heat. This one has a can body (6) that constitutes the heat exchanger (1) at the bottom of the water heater,
An air supply box (7) provided with a perforated plate type gas burner (3) on the upper part of the can body (6) and an air supply chamber (42) on the upper part is arranged. A gas nozzle (31) faces the air supply chamber (42), and a fan is provided above the air supply chamber (42).
(4) is provided. An exhaust pipe (21) is connected to the lower end opening of the heat exchanger (1).

【0013】前記熱交換器(1) は、主にガスバーナ(3)
の燃焼排気の顕熱を吸熱する主熱交換部(1a)と、その下
方に配設され且つ主としてガスバーナ(3) の燃焼排気の
潜熱を吸熱する副熱交換部(1b)とから構成されており、
一方の主熱交換部(1a)は環状のフィン(12)(12)を具備さ
せた通水管(11)から成り、他方の副熱交換部(1b)は前記
通水管(11)における主熱交換部(1a)より上流側部分に環
状のフィン(12)(12)を具備させた構成である。尚、副熱
交換部(1b)に発生するドレンは、缶体(6) 下方のドレン
排出口(8) から外部に排出される。
The heat exchanger (1) is mainly composed of a gas burner (3).
The main heat exchange part (1a) which absorbs the sensible heat of the combustion exhaust gas, and the sub heat exchange part (1b) which is arranged below it and mainly absorbs the latent heat of the combustion exhaust gas of the gas burner (3). Cage,
One main heat exchange part (1a) consists of a water pipe (11) equipped with annular fins (12) (12), and the other sub heat exchange part (1b) is a main heat pipe in the water pipe (11). This is a configuration in which annular fins (12) and (12) are provided on the upstream side of the exchange section (1a). The drain generated in the sub heat exchange section (1b) is discharged to the outside from the drain discharge port (8) below the can body (6).

【0014】この実施例では、前記主熱交換部(1a)にお
ける通水管(11)は、三段で構成されて各段が横二列若し
くは三列に蛇行状に曲成されており、他方の副熱交換部
(1b)の通水管(11)は、横三列に蛇行状に曲成された一段
構成である。そして、副熱交換部(1b)側の通水管(11)
(通水管(11)の最下段部分)から水道水を供給して主熱
交換部(1a)側の通水管(11)(通水管(11)の最上段部分)
から湯を取り出すようにしている。
In this embodiment, the water flow pipe (11) in the main heat exchange section (1a) is composed of three stages, and each stage is meandered in two horizontal rows or three rows. Sub heat exchange part
The water pipe (11) of (1b) has a one-stage configuration in which the water pipe (11) is bent in a meandering shape in three horizontal rows. And the water pipe (11) on the side of the sub heat exchange part (1b)
The tap water is supplied from (the lowermost part of the water pipe (11)) and the water pipe (11) on the main heat exchange part (1a) side (the uppermost part of the water pipe (11))
I try to get hot water out of it.

【0015】副熱交換部(1b)における通水管(11)の断面
両側には、断面円弧状の案内板(5)(5)が、該通水管(11)
のフィン(12)(12)と同芯状に配設されており、これらフ
ィン(12)(12)と案内板(5)(5)との間には、所定の間隔が
形成されている。そして、図4に示すように、当該通水
管(11)を包囲する一対の案内板(5)(5)の上端相互及び下
端相互は、該通水管(11)の外径より小さな間隔を置いて
対向しており、これにより、通水管(11)の上方に開放部
(51)(51)が形成されると共に、該通水管(11)下方に開放
部(52)(52)が形成される。尚、断面円弧状に形成された
各案内板(5) の上下方向の中央部相互と、該中央部と缶
体(6) の内壁とは、燃焼排気の流れを実質的に遮断でき
るように密接させている。又、各案内板(5) には、その
上下方向の中央部の若干上方に複数の透孔(55)(55)が穿
設されている。
On both sides of the cross section of the water pipe (11) in the sub heat exchange section (1b), guide plates (5) (5) having arcuate cross sections are provided.
Are arranged concentrically with the fins (12) (12) of the above, and a predetermined space is formed between these fins (12) (12) and the guide plates (5) (5). . As shown in FIG. 4, the upper and lower ends of the pair of guide plates (5) and (5) surrounding the water pipe (11) are spaced apart from each other by a distance smaller than the outer diameter of the water pipe (11). Facing each other, which results in an opening above the water pipe (11).
(51) and (51) are formed, and open parts (52) and (52) are formed below the water pipe (11). It should be noted that the vertical center portions of the guide plates (5), which are formed in an arcuate cross section, and the central portion and the inner wall of the can body (6) substantially block the flow of combustion exhaust gas. Close Further, each guide plate (5) is provided with a plurality of through holes (55) (55) slightly above the center in the vertical direction.

【0016】したがって、ファン(4) から強制給気を行
なうと共にガスノズル(31)からガスを供給してガスバー
ナ(3) を燃焼させて、通水管(11)の最下段部分から水道
水を供給すると、既述従来のものと同様に、ガスバーナ
(3) で生成された燃焼排気は熱交換器(1) の主熱交換部
(1a)→副熱交換部(1b)→排気筒(21)と流れて外部に排出
される。一方、主熱交換部(1a)や副熱交換部(1b)の通水
管(11)内の通水は、ガスバーナ(3) の発生熱量を通水管
(11)やフィン(12)(12)から吸収して、通水管(11)の最上
段部分から湯となって外部に取り出される。このときの
吸熱作用の中で、ガスバーナ(3) の燃焼排気の顕熱を吸
熱する作用は、主に、主熱交換部(1a)で行われており、
副熱交換部(1b)では、主として、ガスバーナ(3) の燃焼
排気を凝縮させてその潜熱を吸熱する作用が行われる。
即ち、副熱交換部(1b)では、主として、顕熱が奪われて
冷却された燃焼排気をその露点温度以下に冷却させるこ
とによってドレンを発生させ、そのときの潜熱を副熱交
換部(1b)に位置する通水管(11)内の通水に吸収させてい
るのである。
Therefore, if forced air is supplied from the fan (4) and gas is supplied from the gas nozzle (31) to burn the gas burner (3) and tap water is supplied from the lowermost part of the water pipe (11). , A gas burner similar to the conventional one
The combustion exhaust gas generated in (3) is the main heat exchange part of the heat exchanger (1).
(1a) → Sub heat exchange section (1b) → Exhaust pipe (21) and then discharged to the outside. On the other hand, the water in the water flow pipe (11) of the main heat exchange part (1a) and the sub heat exchange part (1b) is the amount of heat generated by the gas burner (3).
It is absorbed from (11) and fins (12) and (12), and becomes hot water from the uppermost part of the water pipe (11) and is taken out to the outside. Among the endothermic action at this time, the action of absorbing the sensible heat of the combustion exhaust of the gas burner (3) is mainly performed in the main heat exchange section (1a),
In the sub heat exchange part (1b), the action of mainly condensing the combustion exhaust gas of the gas burner (3) and absorbing the latent heat thereof is performed.
That is, in the auxiliary heat exchange unit (1b), drainage is generated mainly by cooling the combustion exhaust gas that has been deprived of sensible heat and cooled to a temperature below its dew point temperature, and the latent heat at that time is used to generate latent heat at that time. The water in the water pipe (11) located at () is absorbed.

【0017】このとき、通水管(11)上方の開放部(51)(5
1)以外は、案内板(5)(5)同士等が密接状態にされている
ことから、副熱交換部(1b)に送り込まれる燃焼排気は、
該開放部(51)(51)から集中的に流入して通水管の上面に
接触せしめられ、案内板(5)(5)と、通水管(11)及びフィ
ン(12)(12)との間に流入する。すると、案内板(5)(5)の
形状は断面円弧状としてあることから、案内板(5)(5)と
通水管(11)等との間の空間は、通水管(11)等の外形に倣
った形状に形成されているので、当該燃焼排気は通水管
(11)等の外周面に確実に沿って流れることとなる。そし
て、この燃焼排気は通水管(11)の下方の開放部(52)(52)
から排出され、このときに該通水管(11)の下面に集中的
に接触する。したがって、この実施例のものでは、前記
したような、燃焼排気の通水管(11)やフィン(12)(12)の
全周にわたる有効的な接触作用によって、当該副熱交換
部(1b)においては、燃焼ガスが無駄なく凝縮されて、こ
れにより熱効率が向上する。この凝縮作用によって、副
熱交換部(1b)にはドレンが発生するが、通水管(11)やフ
ィン(12)(12)に付着したドレンは上記開放部(52)(52)を
通ってその下方に滴下し、又、案内板(5)(5)の外壁の上
部に付着したドレンは透孔(55)(55)を通って中に入り、
開放部(52)(52)から下方に流下することから、該ドレン
が副熱交換部(1b)に滞留することはない。尚、上記実施
例では、缶体(6) 内に架設される案内板(5)(5)の上半分
が既述技術的手段の項に記載の第1排気集中手段(A) に
相当すると共に、案内板(5)(5)の下半分が第2排気集中
手段(B) に相当する一方、この案内板(5)(5)の全体が排
気案内手段(C) に相当する。
At this time, the open portions (51) (5) above the water pipe (11)
Except for 1), since the guide plates (5) and (5) are in close contact with each other, the combustion exhaust sent to the sub heat exchange section (1b) is
Concentrated inflow from the open parts (51) (51) is brought into contact with the upper surface of the water pipe, and the guide plates (5) (5) and the water pipe (11) and the fins (12) (12) are connected. Flows in between. Then, since the shape of the guide plates (5) (5) is an arcuate cross section, the space between the guide plates (5) (5) and the water pipe (11), etc. Since it is formed in a shape that follows the outer shape, the combustion exhaust gas will flow through the water pipe.
It will surely flow along the outer peripheral surface such as (11). Then, the combustion exhaust gas is released from the open portions (52) (52) below the water pipe (11).
And is in contact with the lower surface of the water pipe (11) at this time. Therefore, in the embodiment, in the auxiliary heat exchange section (1b), as described above, by the effective contact action over the entire circumference of the water pipe (11) and the fins (12) (12) for the combustion exhaust gas. The combustion gas is condensed without waste, which improves the thermal efficiency. Due to this condensing action, drainage is generated in the sub heat exchange part (1b), but drainage adhering to the water pipe (11) and fins (12) (12) passes through the open parts (52) (52). Drain dripping below it, and the drain attached to the upper part of the outer wall of the guide plates (5) (5) enters through the through holes (55) (55),
Since it flows down from the open parts (52) (52), the drain does not stay in the sub heat exchange part (1b). In the above embodiment, the upper half of the guide plates (5) and (5) installed inside the can body (6) corresponds to the first exhaust gas concentrating means (A) described in the technical means section. At the same time, the lower half of the guide plates (5) (5) corresponds to the second exhaust concentration means (B), while the entire guide plates (5) (5) corresponds to the exhaust guide means (C).

【0018】尚、上記実施例は、以下のように変更が可
能である。 .上記実施例では、各案内板(5) を断面円弧状に形成
したが、これを、図5に示す如く断面「く字状」に形成
してもよい。かかる場合も、缶体(6) 内に架設される案
内板(5)(5)の上半分が既述技術的手段の項に記載の第1
排気集中手段(A)に、案内板(5)(5)の下半分が第2排気
集中手段(B) に相当する一方、案内板(5)(5)全体が排気
案内手段(C) に相当する。
The above embodiment can be modified as follows. . In the above embodiment, each guide plate (5) is formed in an arcuate cross section, but it may be formed in a "dogleg" cross section as shown in FIG. Even in such a case, the upper half of the guide plates (5) and (5) installed in the can body (6) is the first part described in the section of technical means.
In the exhaust gas concentration means (A), the lower half of the guide plates (5) (5) corresponds to the second exhaust gas concentration means (B), while the entire guide plates (5) (5) become the exhaust gas guide means (C). Equivalent to.

【0019】又、図6に示す如く、波形板(5a)(5a)を、
副熱交換部(1b)における通水管(11)の断面両側に配設し
てもよい。この場合、波形板(5a)(5a)の凹凸表面に燃焼
排気が衝突してこれが通水管(11)側に集められ、これに
より、熱効率が向上する。そして、このものでは、波形
板(5a)(5a)の上半分が第1排気集中手段(A) に、下半分
が第2排気集中手段(B) に相当する。 .本発明は、主熱交換部(1a)にて主として顕熱を吸収
し、副熱交換部(1b)にて主として潜熱を吸収する形式の
熱交換器はもちろん、主熱交換部(1a)にて顕熱のみを吸
収し、副熱交換部(1b)にて主として潜熱を吸収する形式
のものにも採用できる。何れの場合でも、主熱交換部(1
a)に本発明を実施してもよい。 .上記実施例では、通水管(11)を蛇行状に曲成させて
4段構成となるようにしてその中で、最下段を副熱交換
部(1b)とし他の3段を主熱交換部(1a)としたが、主熱交
換部(1a)の顕熱吸収能力によっては潜熱を吸収する副熱
交換部(1b)の副通水管(11b) は、下から2段・3段等の
複数段となる。
Further, as shown in FIG. 6, the corrugated plates (5a) (5a) are
You may arrange | position on the both sides of the cross section of the water flow pipe (11) in a subheat exchange part (1b). In this case, the combustion exhaust gas collides with the uneven surface of the corrugated plates (5a) (5a) and is collected on the side of the water pipe (11), whereby the thermal efficiency is improved. In this structure, the upper half of the corrugated plates (5a) (5a) corresponds to the first exhaust concentration means (A) and the lower half corresponds to the second exhaust concentration means (B). . The present invention mainly absorbs sensible heat in the main heat exchange section (1a), and a heat exchanger of the type that mainly absorbs latent heat in the auxiliary heat exchange section (1b), as well as the main heat exchange section (1a). It is also possible to adopt a type in which only the sensible heat is absorbed and the latent heat is mainly absorbed in the sub heat exchange section (1b). In either case, the main heat exchange section (1
The invention may be implemented in a). . In the above embodiment, the water pipe (11) is bent in a meandering manner to form a four-stage structure, in which the lowermost stage is the sub heat exchange part (1b) and the other three stages are the main heat exchange parts. Although (1a) is adopted, the auxiliary water exchange pipe (11b) of the auxiliary heat exchange part (1b), which absorbs latent heat depending on the sensible heat absorbing capacity of the main heat exchange part (1a), is a two-stage or three-stage structure from the bottom. There are multiple stages.

【0020】このように、副熱交換部(1b)が複数段に構
成される場合は、下から2段目若しくは3段目等の通水
管(11)から給水してもよい。又、上記実施例の場合も含
めて、湯の取り出しは上から2段目若しくは3段目等か
ら行ってもよい。 .上記実施例では、ファン(4) を給気通路側に設けた
が、これを排気通路(21)側に設けてもよい。 .上記実施例では、給湯器に本発明を実施したが、給
湯器以外にも、加熱された水を循環させる方式の暖房器
等の熱交換装置にも本発明を採用することは可能であ
る。上記何れの場合でも、熱交換装置が具備する熱交換
器は、燃焼排気中の顕熱を吸熱する機能のみを備える形
式でもよい。 .開放部(52)(52)からドレンを円滑に落下させるた
め、該開放部(52)(52)周縁における案内板(5)(5)の下端
縁から、垂下片を垂下させてもよい。
In this way, when the sub heat exchange section (1b) is constructed in a plurality of stages, water may be supplied from the water pipe (11) at the second or third stage from the bottom. Further, including the case of the above embodiment, the hot water may be taken out from the second or third stage from the top. . In the above embodiment, the fan (4) is provided on the air supply passage side, but it may be provided on the exhaust passage (21) side. . Although the present invention is applied to the water heater in the above embodiments, the present invention can be applied to a heat exchange device such as a heater that circulates heated water in addition to the water heater. In any of the above cases, the heat exchanger included in the heat exchange device may be of a type having only the function of absorbing the sensible heat in the combustion exhaust gas. . In order to smoothly drop the drain from the open portions (52) (52), a hanging piece may be hung from the lower end edges of the guide plates (5) (5) at the periphery of the open portions (52) (52).

【図面の簡単な説明】[Brief description of drawings]

【図1】請求項1の発明の概念図FIG. 1 is a conceptual diagram of the invention of claim 1.

【図2】請求項2の発明の概念図FIG. 2 is a conceptual diagram of the invention of claim 2;

【図3】本発明の実施例の説明図FIG. 3 is an explanatory diagram of an embodiment of the present invention.

【図4】案内板(5)(5)の説明図[Fig. 4] Illustration of guide plates (5), (5)

【図5】案内板(5)(5)の他の例の説明図FIG. 5 is an explanatory view of another example of the guide plates (5) and (5).

【図6】波形板(5a)(5a)の説明図FIG. 6 is an explanatory view of corrugated plates (5a) (5a)

【図7】従来例の説明図FIG. 7 is an explanatory diagram of a conventional example.

【図8】他の従来例の説明図FIG. 8 is an explanatory diagram of another conventional example.

【符号の説明】[Explanation of symbols]

(11)・・・通水管 (A) ・・・第1排気集中手段 (B) ・・・第2排気集中手段 (C) ・・・排気案内手段 (11) ・ ・ ・ Water pipe (A) ・ ・ ・ First exhaust concentration means (B) ・ ・ ・ Second exhaust concentration means (C) ・ ・ ・ Exhaust guide means

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 燃焼装置からの排気通路に吸熱用の通水
管(11)を設けた構成の熱交換装置において、通水管(11)
における排気流の上流側の表面に燃焼排気を集めるため
の第1排気集中手段(A) と、該第1排気集中手段(A) か
らの燃焼排気を通水管(11)における排気流の下流側表面
に集めて排出するための第2排気集中手段(B) とを具備
させた熱交換装置。
1. A water exchange pipe (11) in a heat exchange device having a water absorption pipe (11) for absorbing heat in an exhaust passage from a combustion device.
First exhaust gas concentrating means (A) for collecting the combustion exhaust gas on the upstream surface of the exhaust gas flow, and the combustion exhaust gas from the first exhaust gas concentrating means (A) on the downstream side of the exhaust gas flow in the water pipe (11) A heat exchange device comprising a second exhaust concentrating means (B) for collecting and discharging on the surface.
【請求項2】 第1排気集中手段(A) と第2排気集中手
段(B) との間に通水管(11)の断面側壁に沿って燃焼排気
を案内する排気案内手段(C) を通水管(11)の断面両側に
対向配置した請求項1に記載の熱交換装置。
2. An exhaust guide means (C) for guiding combustion exhaust along a cross-section side wall of a water pipe (11) between the first exhaust concentrating means (A) and the second exhaust concentrating means (B). The heat exchange device according to claim 1, wherein the water pipes (11) are arranged to face each other on both sides of the cross section.
JP5305093A 1993-12-06 1993-12-06 Heat exchange equipment Expired - Fee Related JP2729461B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5305093A JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5305093A JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Publications (2)

Publication Number Publication Date
JPH07159079A true JPH07159079A (en) 1995-06-20
JP2729461B2 JP2729461B2 (en) 1998-03-18

Family

ID=17941024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5305093A Expired - Fee Related JP2729461B2 (en) 1993-12-06 1993-12-06 Heat exchange equipment

Country Status (1)

Country Link
JP (1) JP2729461B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015083883A (en) * 2013-10-25 2015-04-30 増山 征男 Gas cooling device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60176367U (en) * 1984-04-24 1985-11-22 石川島播磨重工業株式会社 Heat exchanger
JPH0158039U (en) * 1987-10-06 1989-04-11

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60176367U (en) * 1984-04-24 1985-11-22 石川島播磨重工業株式会社 Heat exchanger
JPH0158039U (en) * 1987-10-06 1989-04-11

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015083883A (en) * 2013-10-25 2015-04-30 増山 征男 Gas cooling device

Also Published As

Publication number Publication date
JP2729461B2 (en) 1998-03-18

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